div class=ts-pagebutton class=gotoPage data-page=1Page 1button div class=ts-imagea href=https:reader042vdocumentssitereader042viewer20220408025e3b72929752205c3b364468html5page1jpg target=_blank img data-url=graphic1-come-down-to-2-ppm-nox-and-5-or-even-2-ppm-ni-13-slip-in-catalysthtmlpage=1 data-page=1 class=ts-thumb lazyload alt=Page 1: Graphic1 - topsoecomcome down to 2 ppm NOX and 5 or even 2 ppm NI-13 slip In catalyst operation the NH3NOx ratio has to be close to stochiometric Therefore ammonia and flue loading=lazy src=data:imagegifbase64iVBORw0KGgoAAAANSUhEUgAAAAIAAAACCAQAAADYv8WvAAAAD0lEQVR42mP8X8AwAgiABKBAv+vAXklAAAAAElFTkSuQmCC data-src=https:reader042vdocumentssitereader042viewer20220408025e3b72929752205c3b364468html5thumbnails1jpg width=140 height=200 adivdivdiv class=ts-pagebutton class=gotoPage data-page=2Page 2button div class=ts-imagea href=https:reader042vdocumentssitereader042viewer20220408025e3b72929752205c3b364468html5page2jpg target=_blank img data-url=graphic1-come-down-to-2-ppm-nox-and-5-or-even-2-ppm-ni-13-slip-in-catalysthtmlpage=2 data-page=2 class=ts-thumb lazyload alt=Page 2: Graphic1 - topsoecomcome down to 2 ppm NOX and 5 or even 2 ppm NI-13 slip In catalyst operation the NH3NOx ratio has to be close to stochiometric Therefore ammonia and flue loading=lazy src=data:imagegifbase64iVBORw0KGgoAAAANSUhEUgAAAAIAAAACCAQAAADYv8WvAAAAD0lEQVR42mP8X8AwAgiABKBAv+vAXklAAAAAElFTkSuQmCC data-src=https:reader042vdocumentssitereader042viewer20220408025e3b72929752205c3b364468html5thumbnails2jpg width=140 height=200 adivdivdiv class=ts-pagebutton class=gotoPage data-page=3Page 3button div class=ts-imagea href=https:reader042vdocumentssitereader042viewer20220408025e3b72929752205c3b364468html5page3jpg target=_blank img data-url=graphic1-come-down-to-2-ppm-nox-and-5-or-even-2-ppm-ni-13-slip-in-catalysthtmlpage=3 data-page=3 class=ts-thumb lazyload alt=Page 3: Graphic1 - topsoecomcome down to 2 ppm NOX and 5 or even 2 ppm NI-13 slip In catalyst operation the NH3NOx ratio has to be close to stochiometric Therefore ammonia and flue loading=lazy src=data:imagegifbase64iVBORw0KGgoAAAANSUhEUgAAAAIAAAACCAQAAADYv8WvAAAAD0lEQVR42mP8X8AwAgiABKBAv+vAXklAAAAAElFTkSuQmCC data-src=https:reader042vdocumentssitereader042viewer20220408025e3b72929752205c3b364468html5thumbnails3jpg width=140 height=200 adivdivdiv class=ts-pagebutton class=gotoPage data-page=4Page 4button div class=ts-imagea href=https:reader042vdocumentssitereader042viewer20220408025e3b72929752205c3b364468html5page4jpg target=_blank img data-url=graphic1-come-down-to-2-ppm-nox-and-5-or-even-2-ppm-ni-13-slip-in-catalysthtmlpage=4 data-page=4 class=ts-thumb lazyload alt=Page 4: Graphic1 - topsoecomcome down to 2 ppm NOX and 5 or even 2 ppm NI-13 slip In catalyst operation the NH3NOx ratio has to be close to stochiometric Therefore ammonia and flue loading=lazy src=data:imagegifbase64iVBORw0KGgoAAAANSUhEUgAAAAIAAAACCAQAAADYv8WvAAAAD0lEQVR42mP8X8AwAgiABKBAv+vAXklAAAAAElFTkSuQmCC data-src=https:reader042vdocumentssitereader042viewer20220408025e3b72929752205c3b364468html5thumbnails4jpg width=140 height=200 adivdiv